Method and apparatus for making fine glass fibers



Nov 22, 1949 c. STALEG@ 2,489,243

METHOD AND APPARATUS FOR MAKING FINE GLASS FIBERS Filed April 2'?, 1944 3 Sheets-Sheet l "Til mi r 5@ im E f Nov. 22, 1949 c. J. sTALEGo 2,489,243

METHOD AND APPARATUS FOR MAKNG FINE GLASS FIBERS Filed April 27, 1944 3 Sheets-Sheet 2 zwl ZVQ Nov. 22, 1949 c. J. sTALEGo 2,489,243

METHOD AND APPARATUS FOR MAKING FINE GLASS FIBRS Filed April 27. 1944 3 Sheets-Sheet 3 *.WWWWJ ELEM] IN V EN TOR. Cha r/c d. Sfakya MYQMMW Patented 1949 METHOD AND APPARATUS FOR MARIN FINE GLASS FIBERS Charles J. Stalego, Newark, Ohio, assigner to Owens-Corning Fiberglas Corporation, a corporation of Delaware Application April 27, i944, Serial No. 533,046

21 Claims. 1

This invention relates to the production of fibrous material andparticularly to the production of glass nbers by engaging glass with a gaseous blast for attenuating the glass continuously to the form of ilne fibers.

The invention provides improvements of the process in which a rod or filament of heat-softenable material such as glass is fed into an intensely hot blast moving at high speed. The rod is melted by the heat of the blast and as it melts is drawn out `into a ber by the force of the blast. lThe blast is formed by burning a combustible fuel and air mixture, preferably a mixture of fuel gas and air, in a chamber that is enclosed save for a relatively small orifice through which the products of combustion are exhausted. The blast thus created converts the glass engaged thereby at a high rate into tine fibers.

It is an object of the present invention to improve this process to enable the production of finer bers at high rates. This is achieved by increasing the rate and degree of attenuation of the glass so that not only may ilner ilbers be produced but the rods or laments from which the fibers are attenuated may be larger with attendant advantages.

It is another object to provide an improved process whereby line glass fibers may be made with a high degree of uniformity and under accurate control of fiber size.

It is another object to increase the eiciency of the fiber-forming process so that very line fibers may be made at relatively low cost. More speciilcally, it is an object to increase the rate of production of fibers and also to increase the rate of production relative to the amount of fuel consumed in forming the blast. The invention accomplishes this rst object by increasing the speed of the blast, and the second; by increasing the number of rods or laments that may be fed concurrently into the blast to be attenuated by the blast. i

The present invention concerns broadly the conception that finer glass bers of greater uniformity may be produced commercially at very favorable rates if the glass rod or filament is fed into an intensely hot blast incertain directions relative to the direction of travel of the blast, the blast being a unitary body of hot gases traveling at high rate.

Previously the glass rod or filament was fed into a melting and attenuating blast formed by two or more converging llames, the direction of feed ci the rod or lament generally bisecting the angle between the converging llames. The

2 illament moved into the melting and attenuating blast in a direction approximately parallel with the direction of travel of the blast.

With this manner of introduction of the iliament into the blast, the attenuating force is, of course, generally lengthwise of the lament being fed into the blast. Consequently:I as soon as the filament softens it begins to elongate under the iniluence of the attenuating force, and to move into the blast at an accelerated rrte. This accelerated movement of the lament carries the iilament through the portion of the blast adjacent the origin ofthe blast, which is at the highest velocity and highest temperature, at such a rapid rate that the full heating and attenuating `effect of the blast may not be realized. As a and especially not while in the portion of the blast that is at the highest temperature and velocity. The highest degree of attenuation. the iinest fibers, and the highest possible rate of production are consequently not always realized.

It has been found that advantages by way of increased eiiiciency, greater uniformity of the ilbers, and better control of the degree of attenuation are realized if the glass rods or illaments are fed into the blast in a direction that is at substantially a right angle to the direction ofl travel of the blast. There are believed to be several reasons why improved operation results from this manner of feeding.

In the rst place, the attenuating force is normal to the filament and there is therefore little tendency for the lament to elongate until the glass reaches the temperature and viscosity at which attenuation eiciently takes place. Secondly, the temperature gradient along the portion y of the illament entering the blast is highestwhen the filament enters the blast at a right angle, and the lament passes from the solid state to the attenuation viscosity at such a high rate that the intermediate softened state where lengthening or other deformation can occur exists for a time so short that it has little if any effect on the operation. Furthermore, the attenuation temperature and viscosity are reached as close las possible to the point along the length of the blast at which the filament is fed into the blast, which in the interest of eillciency is as close as possible to the point of origin of the blast. It follows that the iiiament fed at a right angle into the blast is raised to the attenuating temperature While in the part of the blast that is hottest and at the l described in more detail with reference to the drawings, in which:

Figure 1 is a diagrammatic elevational view Y of one type of apparatus for carrying out the present invention;

Figure 2 is a horizontal cross-sectional view taken on the line 2--2 of Figure 1 and with the burner broken open and shown partly in section; 'Figure 3 is an enlarged elevational detail view showing a modified form of filament guide, and partly in cross-section;

Figure 4 is a cross-sectional detail view taken in the plane of the line 4-4 of Figure 3;

Figure 5 is -a bottom plan schematic view illustratingthe manner of attenuation of the present invention;

Figure 6 is an elevational view showing a modincation of the apparatus employed to perform the present invention, and partly in cross-section;

Figure 9' is a diagrammatic elevational view vshowing another modification of the apparatus employed in the present invention;

4 from a right angle has very little eil'ect on the mode of attenuation so that a high degree of accuracy in the relation of the guide for the filaments to the blast is not required.

The blast is formed preferably by a burner of the type illustrated at 33. This burner comprises a sheet metal shell Il enclosing a refractory Figure 'I is a cross-sectional view of the same Figure 10` is a fragmentary bottom view. ofjI the bushing forming part of the apparatus illustrated in Figure 9;

Figure 1l is a cross-sectional view taken on the line I i-I I of Figure 9; and

Figure 12 is a side elevational view of a portion of the apparatus of Figure 9.

Although the invention will be particularly described for the production of fine fibers from glass, since it is primarily for this purpose that the invent on has been developed, other mabody 31 having a chamber 38 therein. One end of the chamber is formed by a wall 39 having a plurality of lpassages 4| extending therethrough. The other end of the chamber is formed by a wall 42 having a port 43 therein. This port is of substantially less cross-sectional area than the cross-sectional area of the chamber 38. being usually about Ya to the area of the chamber.

A combustible gaseous mixture, for instance a mixture of fuel gas, either natural or manufactured, and air is fed to the burner through a p1pe 46 that connects with an inlet chambery 41 formed between'the end of the sheet metal casing and the wall 39 of .the refractory body. From the inlet chamber 41 the combustible gaseous mixture passes through the orifices 4i Vand into the chamber 38 where it is ignited. The products of combustion from the gas burned in the chamber 38 pass through the port 43 and are here accelerated, due to the restricted area of the port, to create a high speed blast of intense heat capable of melting and attenuatiug the filaments 23 to'very fine fibers at a high rate.

At the beginning of the operation the gaseous mixture is fed into the chamber 38 at velocities below the rate of flame propagation of the mixture in the atmosphere, but as the refractory walls heat up the rate of feed of the gas intol the chamber is increased above this rate. 'I'he aim, in the interest of highest efficiency, is to feed as much gaseous mixture into the chamber as terials having the properties of being softened when heated and while softened capable of being attenuated, for instance, most thermoplastic resins, may also be converted to fibers by practicing the present invention.

Referring to Figures l to 4, the apparatus comprises a feeder or bushing 2i for feeding a plurality of streams 22 of molten glass that are attenuated into glass filaments 23 by coacting rollers 24, 25 driven by any suitable means. The

'laments emerging from between the rollers pass through grooves 26 cut in one face of a vertically disposed guide plate 2l. The function of .the grooved plate is to guide the filaments in the desired path and maintain them in definite spaced relation.

At the lower end of the plate 21 the `filaments feed into a high speed gaseous blast 29 moving in a, path that is substantially at a right angle to the direction of feed of the filamentsinto the` blast. The blast is intensely hot so that as the filaments move into the blast they are melted and the molten glass is drawn out by the force of the blast into fine glass fibers. The fibers are borne by the blast to a suitable collecting means such as an endless foraminous conveyor 30 travcling over a suction box 3| that causes a fiow of air through the conveyor to aid in deposition of the bers in the form of a mat 32.

The angular relation between the blast and the filaments may be varied to some extent without seriously affecting the operation. Generally, deviations of about 5 or 10U in either direction possible without causing the combustion to become unstable or take place at the outside of the chamber or to cease altogether. l

The guide 21 for guiding the filaments' in spaced paths into the blast utilizes the force of the blast upon the filaments to maintainV the filaments within the grooves 25 of the guide. To more positively maintain the fibers in their proper posi- `tion at all times the modified guide illustrated in Figures 3 and 4 may be employed. This guide is' in the form of a plate divided into two sections 5| and 52 along a substantially central plane. The inner face of the section 5| of the plate is provided with grooves 53 which form guiding passages for the filaments. Intermediate their ends the passages may be deflected so that the lower portion 56 of the passage is at a slight angle to the upper portion of the passage. As a resultI the filaments passing through the payssage are bent slightly, and the resiliency of the l filaments causes them to be urged against the outer edge 54 of the bottom portion of the passage. The guide is so mounted with respect to the burner 33 that the force of the blast from the burner urges the filaments in the same direction that they are urged by their tendency to straighten out in the passage. As a result any tendency of the filaments to move about under the action of the blast is overcome and they feed into the blast in a fixed path.

As the filaments feed into the blast they are quickly melted by the heat of the blast and the molten glass is drawnout by the forcev of the blast into very fine glass fibers.

This action is illustrated diagrammatically Yin Figure 5. The end of each filament 23 as it melts forms a small body 8| of molten glass that is sans and at the highest velocity and the small body of molten glass is held by the filament in this part of the blast so that the blast may act on the molten glass and draw it out. Because lci' Vthe intense heat of the blast the attenuation extends over a relatively great distance so that the molten glass is drawn down to a substantial degree. This manner of feeding the filaments into a blast of intensely hot` gas permits the formation of fibers as small as one hundred-thousandth of an inch or less in diameter, and further provides a high degree of uniformity of these fine fibers.

The size of the fibers attenuated by the gaseous blast may be varied in several ways, e. g., by varying the force and heat of the blast, by varying the sizeof the primary laments, or by varying the rate at which primary fllaments are fed into the blast. Usually, high efficiencies are achieved by feeding primary filaments of from .005 to .010 inch in diameter into the gaseous blast at rates of from 8 to 18 feet per minute to produce blast-attenuated fibers of from .00001 to .00010 inch in diameter. Other sizes and rates may be resorted to without, of course, departing from the invention, these figures being given primarily for purposes of illustration to aid in understanding the invention.

It is evident from these examples that by the present invention it is possible to achieve a degree of attenuation accounting for a reduction in size of the primary iilaments of as high as 500 times. As a consequence, material advantages are realized due to the use of larger primary fi1a ments and the greater ease with which these larger filaments may be produced and operated on in the process.

Figures-6 and 7 show a modified form` of apparatus in which a standard 6| is mounted on a suitable base. A pipe 82 passes through an opening in the standard to be supported thereby and is provided at its forward end with a burner |33, which may be similar in all respects to the burner 33. Beneath the burner there is a plurality of horizontally disposed tubes 64 bent substantially 90 degrees at their forward end so that the ends of the tubes are directed upwardly toward the blast issuing from the burner |33. A bracket Si is suitably clamped to the tubes to maintain them in aligned position and the tubes are clamped adjacent their rear ends in a clamp 81 secured by means of a bracket 63 to the standard 6|.

Spaced rearwardly from the standard 3| a guide block 1| is mounted on the face and provided with a plurality of slots 12 through which the filaments pass. Between the guide 1| and the ends of the tubes 64 a pair of coacting feeding rolls 13, `I4 are mounted on a bracket fastened to the standard. The guide 1| is for the purpose of maintaining the filaments aligned with the tubes 64 as the filaments pass through the rolls ity of streams 11 oi' molten glass and these streams are attenuated to filaments Il by suitable means such as the rollers- 13, 14.

As in the case of the filament guides shown in Figures 1 and 3, the forward ends of the tubes I4 are bent to such an angle that the filaments passing through' the tubes enter the blast. at substantially a right angle and the tendency of the filaments to straighten out urges the ends of the filaments against the forward edge of the end of the.pasages through the tubes so that the filaments are directed through xed paths into the blas In Figure 8 is illustrated a modified form of burner. In this form the port of the burner 233, instead of being formed as an elongated slot, is in the form of a series of spaced orifices 35. The orifices are shown as being substantially diamond-shaped but they may be circular, oval or rectangular if desired. The diamond shape is preferred, however, as permitting closer spacing of the orifices.

With this form of orifice the products of combustion resulting from ignition of the combustible gaseous mixture within the burner are divided into a plurality of spaced .blasts of increased velocity. The'filaments 23 are fed into the individual blasts preferably centrally thereof to be melted and attenuated into fine fibers. In this way the highest velocity of the blast is in the immediate vicinity of the filaments so that the efficiency of the operation is increased..

l Figures 9, 10, 11 and 12 illustrate a modification of the invention by which an increased rate of production is achieved. In this form of the invention the feeder or bushing 3|! is provided with a plurality of orifices for flowing streams of molten glass. The orifices of one series, for instance the row 3N, are of a slightly larger diameter than the orifices of the other series or row 320 so that the streams of molten glass flowing from the orificesare of relatively different diameters. As these streams are attenuated into filaments 32|, 322 by the rollers 324, 325, the filaments are likewise of relative different diameters, the larger orifices of course resulting in the larger filaments 32|. For present purposes, the difference in diameter of the filaments may be in the order of .001 to .003 of an inch, and the different size filaments are preferably slightly above and below the diameter of the filaments required to produce the desired size fibers so that the average diameter of the fibers made from these filaments of different size will closely approximate the desired diameter.

One large and one small filament are fed as a pair through a passage 326 in a guide 321 and are fed in this relation into the blast from the burner 333. As illustrated in Figure 12, the smaller filament is melted and attenuated by the blast from the burner at the point slightly above the point at which the larger filament is melted and attenuated. Also, the smaller filament is flexed by the force of the blast slightly more than the larger filament so that the points where two adjacent filaments are melted and attenuated are spaced apart a small distance lengthwise of the blast as well as vertically. Since the melting and attenuation of the two filaments occurs at spaced points, the two filaments may be fed into the blast in much closer side-by-side relation than if they were the same size and consequently were melted and attenuated at points that were equal distances within the blast. In the latter case the accepts spacing necessary to prevent interference between thc two filaments as they were melted would have to be provided solely by the lateral spacing of the filaments, and as a result fewer filaments could be fed into a blast of given size than may be fed following the present invention.

This manner of feeding relatively different size filaments into the blast may be practiced either with a single blast emanating from a' burner orifice of slot form. or with a series of spaced blasts emanating from a burner oriilce in the form of closely spaced ports as shown in Figure 8. In the latter case, two or more differently sized filaments may beffed into each blast of the series.

' Various modifications may be made within the spirit of the invention and the scope of the claims.

I claim:

1. The process of making glass fibers which comprises forming a gaseous blast having a temperature exceeding the attenuating temperature of glass and having a velocity that will draw out the heated glass into fibers, feeding an elongated body of glass in solidified state lengthwise into the blast from one side thereof and along a path extending transverse of the direction in which the blast travels after it passes the place of entry of said body into the blast, progressively heating the advancing end ofthe elongated body of glass to attenuating temperature by the heat of the blast and drawing out the heated end of/ the body in a direction transverse of the feeding direction of the body entering the blast into a fine glass ber by the force of the blast, and maintaining the heated glass as it is being drawn out integral with the elongated body of glass to cause one end of. the heated glass at the advancing end of the body to resistthe drawing-out action of said blast so that the heated glass is drawn out to a, fine fiber by the blast. f

2. The process of making glass fibers which comprises substantially completely burning a combustible mixture of gases within a chamber and discharging the burned gases from the chamber, introducing the mixture of gases into the chamber at such a rate in relation to the volume of. the chamber and restricting the discharge of burned gases from the chamber to such an extent with respect to the quantity of gas burned within the chamber as to force` the burned gases from the chamber in the form of a blast having a temperature exceeding the attenuating temperature of glass and having a velocity that will draw out the heated glass into fibers, feeding an elongated body of glass in solidified state lengthwise into the blast from one side thereof and along a path extending transverse of the direction in which the blast moves after it passes the point of entry of the body into the blast, heating the advancing end of the glass body to attenuating temperature bythe heat of the blast and by the force of the blast drawing out the heatedglass into fibers in a direction transverseV of the length of the glass body, and maintaining the heated portion of the glass body as it is being drawn out integral with the elongated body to cause one end of the heated glass to resist the drawing-out action of said blast so that the heated glass is pulled out to a fine ilbcr by the blast.

3. The process of making fine glass fibers which comprises feeding a combustible mixture of fuel and combustion-supporting gas into a first zone of a plurality of zones associated in series, substantially completely burning the fuel within the first mne, passing the products of combustion from said zone and into and through a second [s zone at a temperature that is above the attenmting temperature of the glass and at a velocity that will draw the glass continuously into fibers when the glass is subjected to the heat of the said products of combustion in said second zone, feeding an elongated body 0f glass endwise into the second zone through a path laterally ofi'set from said first zonel said feeding being in a direction that is transverse of the direction of travel oi' the products of combustion through said second zone after they pass the place of entry of the elongated body' into the zone, heating'the advancing end of the body of glass by the heat of the products of combustion in said zone to a temperature sufllcient to cause the glass to be drawn out by the velocity of the products of combustion passing through the zone, and attenuating the glass into fibers by the force of the products of combustion passing through said zone.

, 4. Apparatus for attenuating glass into fibers comprising, a burner having a combustion chamber within which a combustible mixture of gas is adapted to be burned and having an outlet opening from which is discharged a single blast of the products of the combustion in said chamber. said outlet opening having a cross-sectional area sufllciently smaller than the cross-sectional area of the space within which the gaseous mixture is burned to provide in a zone at the discharge side of the opening a blast that has a temperature which' exceeds the attenuating temperature of the glass and through which the blast moves at a velocity that will draw out the heated glass into fibers, and means for feeding a body of glass into the blast from one side thereof and along a path laterally oiset from said combustion chamber and extending transversely of the direction of travel of the blast after it passes the place of entry of the body of glass into the blast, said path of feeding of the body of glass intersecting the blast in proximity to the outlet opening of the combustion chamber.

5. The method of making fine glass fibers .which comprises feeding a plurality of closely spaced parallelly arranged glass filaments of relatively different diameters into a gaseous blast tha-t is at a temperature suiliciently high to melt the iilaments and that moves at high velocity, said feeding direction being transversely of the direction of travel of the blast, the relative size of said filaments resulting in attenuation thereof at different extents of penetration of the filaments into the'blast to thereby space apart the points where attenuation occurs within the blast.

6. The method of making fine glass fibers which comprises feeding a plurality of closely spaced parallelly arranged glass filaments into a gaseous blast thatA is at a temperature sufllciently high to melt the filaments and that moves at high velocity, said feeding direction being transversely of the direction of travel of the blast, said fllaments being in pairs with the filaments of each pair being of relatively different diameters.

7. The method of making glass fibers which comprises ilowing a plurality of streams of molten glass of relatively different cross-sectional areas, continuously drawing out and solidifying said streams to form filaments of relatively different diameters, feeding said filaments as they are attenuated in side by side closely spaced relationship into a gaseous blast of intense heat and moving at high velocity, the direction of feed of the filaments into the blast'being transverse to the direction of travel of the blast, and melting and attenuating said illaments by the heat and Y, e force of tneb1astlltne'cre1atlye size of said niaments resulting in' 'attenuation thereof at diierent extentsof pedetrattori ,of rthe"filaments into the meseta thereby spaeeapart the points where:

attenuation occurs withinthe blast.

8. `Apparatus for making linebers comprising` a burner for formingvja high, speed4 gaseous `blast of intense heat, means for flowing a.1 stream of molten lglass from a' supply thereof, and 'means for engaging said'stream andmovable in direc tions generally away `from the'lsaid supply to attenuate the stream to a lament and in a direction thatli's generally transverse of the direction of1 the blast to feed the filament Vas it is attenuated into the gaseous blast in a direction atsubstantially a right angle tothe direction of travel of l'the blast.

9. Apparatus `for making vfine glass ilbers corn--V prising a feeder for` flowing streams of molten glass, means for attenuating said streams spaced from said feeder at a distance suiiicient to cause illaments are attenuated concurrently Y byv`v heat and force ot "said"spaced.blasts.

v,13. Apparatus` `for Lmaking Vglass bers which comprisesmeans fo`r flowing a'stream `of molten theattenuated streams to solidify 1n the form of 10. Apparatus for-making ne glass fibers comprising a feeder for owingstreams" of molten glass, meansforattenuat'ing Vsaid streams spaced fromsaid feeder at a distance'suffcent to cause the"attenuated streams to' solidifyin. the form of glass illaments, a burner including an enclosed chamber in which a combustible gaseous mixture is burned and a restricted port through which" the products of combustion pass from said chamber intothe atmosphere to form a high speed gaseous blastj'of intenseV heat, and a' guide for the filaments adjacent'fthe port ofV said burner I arranged tov guidefthe laments into' the gaseous blast discharging frm :said port, 'the 4filament-contacting portion of said guide-in the vicinity 'of the blast being at substantially a right angle to the direction of travel of the blast.

11. Apparatus for making fine glass fibers which comprises a burner including an enclosed chamber in which a combustible gaseous mixture is burned, said burner having a series of` spaced apart exhaust ports leading from said chamber to the atmosphere for exhausting the products of combustion from the chamber to form a plurality of blasts of intensely hot gas moving at high velocity, and means for feeding a. plurality of elongated bodies of glass into said blasts with the bodies individual to said blasts, whereby said bodies are attenuated concurrently by the heat and force of said blasts.

12. Apparatus for making ne glass fibers which comprises a burner including an enclosed chamber in which a combustible gaseous mixture is burned, a series of'parallelly arranged laterally spaced vertically elongated passages leading from said chamber to theatmosphere for exhausting the products of combustion from the chamber to form a plurality of spaced blasts of intensely hot gases moving in parallel paths at high velocity, and means for feeding a plurality of elongated bodies of glass into said spaced blasts with the laments indlvldualto said blasts, whereby said 75 glass, means for attenuatitlgv said stream continu-'5l ously to continuously form la solid glass filament' and to advance the n'lament inthe direction ot its length, a burner for formi ng a high speed gaseous blast of intense heat..and aguide be*-v tween said att'enuatingfmean's and said-burner for guiding said advancing illamentinto the blast;v at a point adjacent the burner and in.a,direction at substantially a right angle 4to e the directionz of movement of said blast.

14. Apparatus for making `Vglass bersgwhich comprises a feeder for molten glass and having orifices therein of relatively different sizes for flowing a plurality of molten glass streams of relatively diierent cross-sectional areas, attenuating means for engaging the streams and continuously drawing out said streams all at the same rate to form fllamentsof relatively different4 diameters and for feeding said laments as they are attenuated in side by side closely `spaced relation into a gaseous blast of intense heat and moving at high velocity, whereby the laments are melted by the heat of the blast at points spaced apartinthe direction of feed of the lilaments and attenuated by the forceof the blast.

15. Apparatus for making glass fibers which i comprises afeeder for molten glass and having orifices therein of relatively different sizes for flowing a plurality of molten glass streams of relatively dilerent cross-sectional areas, attenuating mean-s for engaging .the streams and confilaments of different size aremelted. by ltheheat of the blast atpointsgspaced apart in the'direc-l tion of feed of thefllaments and attenuated by:V

the heat and force. of the blast.

16. The process of makingiibers from heatt softenable materialwhich comprises owingia stream of molten material from a supply body of molten material and solidifying the stream to form a filament, attenuating the stream of molten material prior to its solidication by ap plying a pulling force on the filament, and attenuating the filament thus formed to form bers by projecting the lament endwise into a gaseous blast having a temperature in excess of the softening temperature o1' the material and having a velocity sufficient to draw out the softened material into bers. l

1'7. The process of making glass fibers which comprises flowing a stream of glass from a supply body of molten glass and solidifying the stream to form an elongated body of solid glass, burning a combustible gaseous mixture in a conned space and passing the products of combustion from said space and then through a zone at a temperature in excess of the softening temperature of the glass, progressively softening the advancing end' of said body by feeding the body endwise into said zone along a path of travel extending transversely of the direction of movement of said products of combustion through said zone, and attenuating the softened body into libres by the force of said products of combustion.

18. Apparatus for making glass fibers comprising a feeder having means for flowing a stream of molten glass, means for attenuating the stream spaced from the feeder a distance sumcient to cause the attenuated stream to solidify in the form of a filament before being engaged by the attenuating means, a gas burner having means for discharging the products of combustion in the form of a blast having a temperature in excess of the softening temperature of the glass and having a velocity suillcient to draw out the glass into fibers, said burner being so located with respect to the attenuating means that the filament leaving the attenuating means is fed by the latter into said blast along a path extending transversely of the direction of iiow of the blast.

19. Apparatus for making bers from heatsoftenable material, comprising a feeder having means for flowing a stream of the material in molten state, means for engaging the stream and feeding the stream along a predetermined path, said feeding means being spaced from the feeder a distance suillcient to cause the stream to solidify in the form of a filament before being engaged by the feeding means, a burner having a chamber in which a combustible gaseous mixture ls burned and having an outlet opening through which the products of combustion are discharged in the form of an intensely hot high velocity blast, and means between the feeding means and blast for guiding the filament into the blast along a path extending transversely to the direction of iiow of the blast.

20. The process of making fibers from heatsoftenable material which comprises burning a combustible gaseous mixture in a confined space and passing the products of combustion from said space through a zone in the form of a gaseous blast having a width substantially greater than its depth and having a temperature in said zone exceeding the softening temperature of the material, feeding a plurality of elongated bodies of the material in side by side relation endwise into the blast in said zone with the elongated bodies spaced laterally from each other crosswise of the blast, guiding the elongated bodies into the blast along a path extending substantially normal to the blast, moving the products of combustion Number 12 through the zone at a velocity sumciently high to draw out the material at the advancing ends of said bodies, and attenuating the material into fibers by the force of the blast passing through said zone.

21. Apparatus for attenuating glass into fibers comprising, a burner having a combustion chamber within which a combustible gaseous mixture is adapted to be burned and having an outlet opening of a width several times greater than its depth and through which the products of combustion are discharged in a wide, ribbon-like blast, said outlet opening having a cross-sectional area sufflciently smaller than the cross-sectional area of the space within which the gaseous mixture is burned to provide a'zone at the discharge side of the opening in which the temperature of the blast exceeds the softening temperature of the glass and through which-the blast moves at a velocity suillciently high to draw out the softened glass into a fine fiber, means supported exteriorly of the burner for feeding a plurality of glass rods into said zone at such a rate that the rods entering the zone are melted in the blast and the molten glass is drawn out into fibers by the force of the blast, and a guide restraining movement of the rods into the blast along a path extending substantially normal to the blast and having means for positioning the rods in lateral spaced relation across the width of the blast.

CHARLES J. STALEGO.

REFERENCES CITED The following references are of record in the ille of this patent:

UNITED STATES PATENTS Name v Date 1,008,204 Seghers Nov. 7, 1911 1,049,314 Neil Dec. 31, 1912 1,157,984 Herkenrath Oct. 26, 1915 1,689,551 Hammond Oct. 30, 1928 2,068,203 Simpson Jan. 19, 1937 2,133,235 Slayter Oct. 11, 1938 2,133,238 Slayter Oct. 11, 1938 2,175,225 Slayter Oct. 10, 1939 2,228,150 Norman, Jr Jan. 7, 1941 2,291,289 Slayter et al. July 28, 1942 2,335,135 Staelin Nov. 23, 1943 

